JPS61293376A - Sheetlike food material produced through extrusion cooking process - Google Patents
Sheetlike food material produced through extrusion cooking processInfo
- Publication number
- JPS61293376A JPS61293376A JP60133098A JP13309885A JPS61293376A JP S61293376 A JPS61293376 A JP S61293376A JP 60133098 A JP60133098 A JP 60133098A JP 13309885 A JP13309885 A JP 13309885A JP S61293376 A JPS61293376 A JP S61293376A
- Authority
- JP
- Japan
- Prior art keywords
- animal
- sheet
- raw materials
- food
- vegetable
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- General Preparation And Processing Of Foods (AREA)
- Jellies, Jams, And Syrups (AREA)
- Formation And Processing Of Food Products (AREA)
- Grain Derivatives (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は動植物性蛋白質原料と澱粉質原料を主原料とし
、動植物性蛋白質原料ならびに各種可塑剤、調味料、香
辛料、着香料、着色暮等を副原料とした混合物を、エク
ストルージョン・クツキング工程を経て製造するシート
状食品素材類に関する。[Detailed description of the invention] [Industrial application field] The present invention uses animal and vegetable protein raw materials and starch raw materials as main raw materials, and uses animal and vegetable protein raw materials as well as various plasticizers, seasonings, spices, flavoring agents, colorants, etc. The present invention relates to sheet-shaped food materials manufactured by using a mixture using `` as an auxiliary raw material through an extrusion/cutting process.
食品のなかに含まれる水分には、遊離水とよぶ水分およ
び結合水とよぶ水分の種類があるが、この他に、食品を
密閉容器に入れて放置したときの器内の湿度と、その温
度における飽和湿度との比を示す水分活性(At)があ
り、水分活性(At )は食品の貯蔵性と関係があり、
水分活性(At)の高い食品は微生物の被害を受けやす
いとされている。(桜井芳人纒「総合食品事典」第3版
、第467〜468頁「水分」)
本発明者らは、食品の保存性について研究を続けてきた
が、その研究において、軟らかい食品は、その水分活性
(Ay)が高く、貯M件に乏しいが、水分活性(At
)が低く、充分な貯蔵性を有する食品は、食品自体が硬
くなる傾向があることを見出し、水分活性(At)が低
く、すぐれた貯蔵性を有する食品であっても、軟らかい
食品素材を製造することを企図して、さらに研究を重ね
、動植物性蛋白質原料と澱粉質原料を主原料とし、これ
に動植物性油脂類原料、ならびに各種可塑剤、調味料、
香辛料、着香料、着色料等を副原料とした混合物を、こ
れまでにプラスチックスの加工や少水分系の食品原料の
膨化に用いられてきたエクストルーダーを使用するエク
ストルージョン・クツキング工程にかけ、食品原材料の
混合物に物理化学的熱反応を起させると、水分活性(A
t)が低く、すぐれた貯蔵性を有していても、軟らかい
組織を有する食品が得られることを見出し、この知見に
もとづいて本発明に到達した。There are two types of moisture contained in food: free water and bound water. In addition, there are two types of moisture contained in food: the humidity inside the container when the food is left in an airtight container, and its temperature. There is a water activity (At) that shows the ratio of the saturated humidity at
Foods with high water activity (At) are said to be susceptible to damage from microorganisms. (Yoshihito Sakurai, Comprehensive Food Encyclopedia, 3rd edition, pp. 467-468, "Moisture") The present inventors have continued to research the preservation properties of foods, and in their research, they found that soft foods Although water activity (Ay) is high and M storage is poor, water activity (At
) and have sufficient storage stability, the food itself tends to become hard, and even if the food has low water activity (At) and excellent storage stability, it is possible to produce soft food materials. With this in mind, we conducted further research and developed a product that uses animal and vegetable protein raw materials and starch raw materials as the main raw materials, as well as animal and vegetable fat and oil raw materials, as well as various plasticizers, seasonings, and
A mixture of spices, flavorings, colorings, etc. as auxiliary raw materials is subjected to an extrusion and packing process using an extruder, which has been used to process plastics and expand low-moisture food materials. When a mixture of raw materials undergoes a physicochemical thermal reaction, water activity (A
It was discovered that a food product having a soft texture can be obtained even if the food product has a low t) and has excellent storage properties, and based on this finding, the present invention was achieved.
本発明の目的は、上記した製品をそのままの状態で他の
食品類に挟んだり、他の食品類を中心にして巻いたり、
他の食品類とともに煮たりして装置出来るとともに、本
製品単独で蒸したり、焼いたり、食用油でいためたり、
食用油で揚げたりして装置することが出来る新しい組織
を有し、多目的利用の可能な食品素材を提供することと
、−白の装置で原材料の搬送と均質混合、搬送の進行に
従って順次温度上昇を伴うクツキング、高温高圧せん断
、押出成型操作を連続して行ない、しかも60〜90秒
でこれらの操作を完了するという省力、省エネルギー製
造法を提供することにある。The purpose of the present invention is to sandwich the above-mentioned product as it is between other foods, wrap it around other foods,
This product can be boiled with other foods, and can also be steamed, baked, or cooked with cooking oil on its own.
To provide food materials that have a new structure that can be fried in edible oil and can be used for multiple purposes; - The white equipment transports and homogeneously mixes the raw materials, and gradually increases the temperature as the transport progresses. The object of the present invention is to provide a labor-saving and energy-saving manufacturing method in which the processes of knitting, high-temperature, high-pressure shearing, and extrusion molding are performed continuously, and these operations can be completed in 60 to 90 seconds.
従来からあるシート状食品としては、スライスチーズ、
スライスハム、海苔等があるが、これらの食品または食
品素材の製造法は、エクストルージョン・クツキング工
程を採用しておらず、埋々の独立した工程を順次組合せ
て完成されるに反し、不法は原材料の予備的混合は公知
方法を採用するが、その後はエクストルーダーのシリン
ダー内をスクリューによって混合原料を搬送し、原材料
をより均質に混合する操作と、原材料の搬送が進むに従
って順次温度を上昇させクツキングして可塑化させる操
作と、可塑化した原材料から発生する水蒸気圧と特殊ス
クリューによって原材料にせん新液型を与える操作とス
クリューの搬送力と発生した水蒸気圧とによって原材料
をノズ」し門番こ強制的に誘導して成形しながら押出す
操作を一台の装置内で連続して実施し、しかもこの連続
した5つの操作を経ることによって原材料に物理化学的
反応を起させ、新しい物性を付与したシート状食品素材
を得ることを特徴としている。Traditional sheet foods include sliced cheese,
There are sliced hams, seaweed, etc., but the manufacturing methods for these foods or food ingredients do not use extrusion/crucking processes, and are completed by sequentially combining many independent processes. A known method is used for preliminary mixing of the raw materials, but after that, the mixed raw materials are conveyed by a screw inside the cylinder of the extruder, and the raw materials are mixed more homogeneously, and the temperature is sequentially increased as the raw materials are conveyed. The operation of plasticizing the raw material by kneading, the operation of giving a new liquid form to the raw material using the water vapor pressure generated from the plasticized raw material and a special screw, and the nozzle operation of the raw material using the conveying force of the screw and the generated water vapor pressure. Extrusion operations are performed continuously within a single device while being forcibly guided and shaped, and through these five consecutive operations, a physicochemical reaction occurs in the raw material, giving it new physical properties. It is characterized by obtaining a sheet-like food material.
本発明は従来プラスチックスの加工及び少水分系の食品
原料の膨化に用いられて来たエクストルーダーを使用し
、食品原材料の混合物に物理化学的熱反応を起させ、従
来見られなかった新しい物性を形成させたシート状食品
素材で、厚みが0.5〜10.0II+s+の範囲内に
あり、また水分含量が5.0〜50.0%の範囲内にあ
る。但し、使用用途によって厚み、水分含量、巾、長さ
は適宜に変更することが出来る。The present invention uses an extruder that has conventionally been used to process plastics and expand low-moisture food raw materials to cause a physicochemical thermal reaction in a mixture of food raw materials, resulting in new physical properties never seen before. It is a sheet-like food material formed with a thickness in the range of 0.5 to 10.0II+s+, and a moisture content in the range of 5.0 to 50.0%. However, the thickness, moisture content, width, and length can be changed as appropriate depending on the intended use.
本発明に用いる主原料のうち、動植物性蛋白質原料は、
魚肉すり身、魚肉落し身、魚介類ペースト、魚介類細断
物、獣鳥肉ペースト、獣鳥肉ひき肉、牛乳または粉乳、
鶏卵汁または乾熾鶏卵、血液プラズマ蛋白、大豆蛋白、
穀類蛋白等のうち一種または二種以上の混合物を用いる
。また主原料の澱粉質は、穀類粉、穀類澱粉、根茎澱粉
等のうち一種または二種以上の混合物を用いる。Among the main raw materials used in the present invention, animal and vegetable protein raw materials are:
Minced fish, ground fish, seafood paste, shredded seafood, animal and poultry paste, ground animal and poultry meat, milk or powdered milk,
Chicken egg juice or dry roasted chicken eggs, blood plasma protein, soybean protein,
One or a mixture of two or more of grain proteins is used. The main starch material used is one or a mixture of two or more of cereal flour, cereal starch, rhizome starch, and the like.
また副原料として用いる動植物性油脂原料としては、動
植物性マーガリン、バター、動植物性油脂、動植物性燐
脂質等のうち一種または二種以上の混合物を用いる。In addition, as the animal and vegetable oil raw material used as the auxiliary raw material, one or a mixture of two or more of animal and vegetable margarines, butter, animal and vegetable oils, animal and vegetable phospholipids, etc. is used.
また可塑剤としては、グリセリン、プロピレングリコー
ル、ゾルビトール、脂肪酸エステル類、水飴、コーンシ
ラヅプ、砂糖シラツブ等のうち一種または二種以上の混
合したものを用いる。As the plasticizer, one or a mixture of two or more of glycerin, propylene glycol, sorbitol, fatty acid esters, starch syrup, corn syrup, sugar syrup, etc. is used.
調味料としては、食塩、糖類を含む天然調味料およびア
ミノ酸類を含む化学調味料、複合調味料類のうち一種ま
たは二種以上の混合したものを用い、香辛料セしては天
然香辛料類および合成調味料類のうち、一種または二種
以上の混合したものを用い、着色料、着香料としては、
天然色素、天然香料類および合成色素、合成香料類のう
ち、一種または二種以上混合して用いる。As seasonings, use one or a mixture of two or more of natural seasonings containing salt and sugars, chemical seasonings containing amino acids, and complex seasonings, and for spices, natural spices and synthetic seasonings are used. Among seasonings, use one or a mixture of two or more, and as coloring and flavoring agents,
One or a mixture of two or more of natural dyes, natural fragrances, synthetic dyes, and synthetic fragrances are used.
以上のうち、主原料となる動植物性蛋白質は、全原材料
重の20〜60%、好ましくは25〜4596を用い、
また澱粉質原料は20〜50%、好ましくは25〜45
%用いる。澱粉系原材料含量が多くなると製品は乾Q状
態のものが得られ、水分の多い蛋白質原料の含量が多く
なれば製品は柔軟な個性または半湿性状態のものが得ら
れる。副原料のうち、動植物性油脂原料は、原材料全型
の2〜15%、好ましくは1096未満の添加が好まし
く、この副原料を多部すると製品の柔軟性は付与される
が、エクストルーダーン・クツキング工程において原料
搬送時に滑り現象を伴ない、せん断が減殺され、製品組
織が軟弱となる。Among the above, the animal and plant protein serving as the main raw material is 20 to 60% of the total raw material weight, preferably 25 to 4596%,
In addition, the starchy raw material is 20 to 50%, preferably 25 to 45%.
Use %. If the content of starch-based raw materials increases, the product will be in a dry Q state, and if the content of water-rich protein raw materials increases, the product will have a soft texture or a semi-moist state. Among the auxiliary raw materials, animal and vegetable oil and fat raw materials are preferably added in an amount of 2 to 15% of the total amount of raw materials, preferably less than 1096%.A large amount of this auxiliary raw material imparts flexibility to the product, but extruder In the shoeing process, slippage occurs during the transportation of raw materials, which reduces shear and weakens the product structure.
また副原料としての可塑剤は、製品の柔軟性と保型性付
与、水分活性(At )の低下を目的として添加される
ものであり、全原材料中の2〜20%、好ましくは5〜
10%の添加が望ましい。Plasticizers as auxiliary raw materials are added for the purpose of imparting flexibility and shape retention to products and reducing water activity (At), and are added in an amount of 2 to 20%, preferably 5 to 20%, of the total raw materials.
Addition of 10% is desirable.
次に本発明製品の製造装置と処理方法について述べる。Next, the manufacturing apparatus and processing method for the product of the present invention will be described.
先づ製造装置は、シリンダー径46m、い=15の二軸
同方向回転方式のエクストルーダーを用いるが、これに
限定されるものではなく、原材料の種類や配合割合なら
びに製品の目的用途の差異により、φ比の異なるものや
、−軸型ならびに異方向回転二軸エクストルーダーを用
いることも出来る。First, the manufacturing equipment uses a two-axis co-rotating extruder with a cylinder diameter of 46 m and a cylinder diameter of 15 mm, but is not limited to this. , extruders with different φ ratios, -shaft type, and biaxial extruders rotating in different directions can also be used.
処理方法は、先づ前記した原材料類を公知の混合または
混練ゆ機で予備的に混合、混練りしておき、これをエク
ストルーダーに付属する原料供給機に移す。この原料供
給機よりエクストルーダーシリンダー円に混合原材料を
毎分500〜2,0009、好ましくは毎分t 、 o
oo〜1,4θOyづつ送り込む。In the processing method, first, the above-mentioned raw materials are mixed and kneaded in advance using a known mixing or kneading machine, and then transferred to a raw material feeder attached to an extruder. The mixed raw materials are fed into the extruder cylinder from this raw material feeder at a rate of 500 to 2,0009 m/min, preferably t, o/min.
Feed by oo~1,4θOy.
シリンダー内のスクリュー回転速度は毎分50〜200
回転、好ましくは80〜120回転とし、原材料投入口
付近の温度は5〜3Q’C%好ましくは2Q’C以下と
し、混合原材料がスクリューによって200 m程度搬
送された付近のシリンダー内温度を60〜90℃、好ま
しくは70〜80℃とし、この部位のスクリューは、原
材料がより均質に混合されるような構造をもったものを
配置する。The screw rotation speed in the cylinder is 50 to 200 per minute.
Rotation, preferably 80 to 120 rotations, temperature near the raw material input port 5 to 3Q'C%, preferably 2Q'C or less, and temperature inside the cylinder near where the mixed raw materials are conveyed about 200 m by the screw to 60 to 120. The temperature is set at 90°C, preferably 70 to 80°C, and the screw in this part is arranged to have a structure that allows the raw materials to be mixed more homogeneously.
原材料がさらに搬送されて、原材料投入口より430順
付近に達した部位のシリンダー内温度を100〜125
℃、好ましくは110〜120℃とし、またこの部位の
スクリューは、成程度せん断を伴なうような構造のもの
を配して原材料に加熱とせん断を与えるようにする。原
材料がさらに搬送されて、原材料投入口より600u付
近に達した部位のシリンダー内温度を130〜160℃
、好ましくは130〜150°Cとし、この部位のスク
リューはより高度なせん断力を原材料に与える構造のも
のを配する。The raw material is further transported and the temperature inside the cylinder is set at 100 to 125 at the point near 430 from the raw material input port.
℃, preferably 110 to 120°C, and the screw in this part has a structure that causes a certain degree of shear to apply heat and shear to the raw material. The temperature inside the cylinder where the raw material is further transported and reaches around 600u from the raw material input port is 130-160℃.
, preferably from 130 to 150°C, and the screw in this region has a structure that provides a higher shearing force to the raw material.
スクリューの爵先端および吐出ノズル内温度は140〜
165℃、好ましくは150〜160℃とし、またこの
部分の水蒸気圧は7〜20Kg/7.好ましくは10〜
15 Ky / ah程度を保持させる。尚、最先端に
配置するスクリューは、スーパーヒートされ、かつ加圧
、せん断された原材料の組織を崩壊させないような構造
のスクリューを配置する必要がある。The temperature at the tip of the screw and inside the discharge nozzle is 140~
The temperature is 165°C, preferably 150-160°C, and the water vapor pressure in this area is 7-20Kg/7. Preferably 10~
Maintain around 15 Ky/ah. Note that the screw placed at the leading edge must have a structure that does not collapse the structure of the superheated, pressurized, and sheared raw material.
製品を吐出させるノズルは、開口部のサイズは厚み0.
3〜10.01LllX巾30〜150鴎、好ましくは
0.5〜5.0 BX 40〜10011j+、ノズル
の深さ30〜150sum、好ましくは80〜110順
のものを用い、シリンダー内部に発生した水蒸倶圧と、
スクリューの回転とによって製品を強制的に、かつ連続
的にノズル口より外部へ吐出させる。外部に吐出した製
品は、シリコン製のベルトコンベアに乗せてロータリー
カッターに誘導して、製品の長さを50〜300 su
s 、好ましくは100〜200 uに裁断し、さらに
ベルトコンベアに乗せて風冷し、品温を20℃以下に冷
却した後、5〜30枚を色装単位として真空包装し製品
とする。The nozzle that discharges the product has an opening size with a thickness of 0.
3-10.01LllX Width 30-150mm, preferably 0.5-5.0B vapor pressure and
By rotating the screw, the product is forcibly and continuously discharged to the outside from the nozzle opening. The product discharged to the outside is placed on a silicone belt conveyor and guided to a rotary cutter to cut the length of the product into 50 to 300 su.
s, preferably into pieces of 100 to 200 μm, and then placed on a belt conveyor and air-cooled to a temperature of 20° C. or lower. After that, 5 to 30 pieces are vacuum-packed as a colored unit to produce a product.
以上述べたように本発明製品は、動植物性蛋白質原料と
、澱粉質原料を主原料とし、動植物性油脂、動植物性燐
脂質、可塑剤、調味料類、香辛料類、着香料、着色料等
を混合して、エクストルーダーシリンダー内に送り込み
、前記したように一台の装置で原材料を搬送し、原材料
のより均質混合、原材料を次第に加温、加圧、原材料に
せん断変形を与え、物理化学的反応を起こさせて、独特
の組織を形成させたシート状製品を吐出させることを特
徴としており、しかも原材料をシリンダーに供給して吐
出させるまでの時間が60〜90秒という短時間で製造
を完了させる省力的で、しかも熱エネルギーが大巾に短
縮出来る製産法を採用している。As mentioned above, the products of the present invention are mainly made of animal and vegetable protein raw materials and starch raw materials, and contain animal and vegetable oils, animal and vegetable phospholipids, plasticizers, seasonings, spices, flavorings, colorants, etc. The raw materials are mixed and fed into an extruder cylinder, and as described above, the raw materials are transported by one device, and the raw materials are mixed more homogeneously, the raw materials are gradually heated and pressurized, and the raw materials are subjected to shear deformation, and physicochemical It is characterized by causing a reaction and discharging a sheet-like product with a unique structure formed, and manufacturing can be completed in a short time of 60 to 90 seconds from supplying raw materials to the cylinder to discharge. We have adopted a manufacturing method that is labor-saving and can greatly reduce heat energy consumption.
本発明製品は、厚みが0.3〜11.0m、巾30〜1
55鴎で独特の組織をもつシート状食品素材であるが、
原材料中の水分ならびに油脂類、流動性可塑剤の含有量
を増加させた場合には、かなり柔軟性ある半湿のシート
状食品素材となり、この状態の製品の水分活性(At)
値は0.8〜0.99の範囲にあり、また原材料のうち
澱粉質含量および粉末状の蛋白質含量が大きく、水分含
量が少ない場合には、比較的硬いシート状食品素材とな
り、この状態の製品の水分活性(At )値は0・60
−0.80の範囲となる。The product of the present invention has a thickness of 0.3 to 11.0 m and a width of 30 to 1 m.
55 Ume is a sheet-like food material with a unique structure,
When the content of water, fats and oils, and fluid plasticizers in the raw materials is increased, it becomes a fairly flexible semi-moist sheet food material, and the water activity (At) of the product in this state increases.
The value is in the range of 0.8 to 0.99, and if the starch content and powdered protein content of the raw material is high and the water content is low, the sheet-like food material will be relatively hard, and in this state. The water activity (At) value of the product is 0.60
-0.80 range.
これらの食品素材の利用用途としては、上記したかなり
柔軟性のある半湿状態のものは、パンサンドウィッチの
ように他の食品と食品の間の挟み材料や、他の食品を中
心にして本発明食品素材で巻いて供食することが出来る
。The use of these food materials is as follows: those in a semi-moist state, which are quite flexible, as mentioned above, can be used as sandwiching materials between other foods, such as bread sandwiches, and other foods. It can be wrapped in food materials and served as an offering.
また、上記した硬いシート玖のものは、水に浸けるか、
或いは沸騰水中で2〜3分間ボイルして冷却するか、ま
たは蒸気中で10〜15分間蒸して、他の食品と食品の
間に挟み材料また他の食品を巻き込んで装置出来るとと
もに、水浸けしたもの、ボイルしたもの、蒸したものを
食用油でいためたり、食用油で揚げたり、さらには他の
食品と煮込んで供食することも可能である。Also, if you use the above-mentioned hard sheet, you can soak it in water or
Alternatively, it can be boiled in boiling water for 2 to 3 minutes to cool down, or steamed in steam for 10 to 15 minutes, and can be sandwiched between other foods or other foods can be wrapped in the device, and can be soaked in water. It is also possible to prepare food, boil it, steam it, fry it in edible oil, fry it in edible oil, or even simmer it with other foods.
このように本製品は、惣菜ならびにスナヅク食品等、多
目的な食材として利用することをねらいとしており、従
来者えられなかったような組織製品を供給し、時代にマ
ツチした嗜好食品を提供することが出来る。In this way, this product aims to be used as a multi-purpose ingredient such as side dishes and snack foods, and it is possible to supply tissue products that were not available before, and to provide taste foods that are in line with the times. I can do it.
さらに本発明食品素材のうち水分活性(At)値が0.
60〜0.92の範囲にあるものは貯蔵性がある。この
貯蔵性は製造時の高温、高圧処理により、原材料中の微
生物が製造直後において殆んど殺菌されていることにも
起因する。Furthermore, among the food materials of the present invention, the water activity (At) value is 0.
Those in the range of 60 to 0.92 have shelf life. This shelf life is also due to the fact that most of the microorganisms in the raw materials are sterilized immediately after production due to high temperature and high pressure treatment during production.
実施例 !
(’1 )原材料の配合割合および混合法は下記のよう
に実施した。Example ! ('1) The blending ratio and mixing method of raw materials were as follows.
原 材 料 配合割合 配合重量
すけとうすり身 4o% S、OKg強力小麦粉
34 6.8グリセリン to
2.0脱脂粉乳 51.0
大豆レシチン 51.0
プルラン 20.4
食塩 20.4
化学調味@ 1 o、z、天然香辛
料 !0.2
it 100 20.0上記原材料
の混合は、半解凍したすけどうすり身を約1 cm角に
裁断し、さらにフードカッターで細切した後、らいかい
機に移し他の原材料を順次添加して20分間混練りした
。Ingredients Mixing ratio Mixing weight Walleye surimi 4o% S, OKg strong wheat flour 34 6.8 Glycerin to
2.0 Skimmed milk powder 51.0 Soybean lecithin 51.0 Pullulan 20.4 Salt 20.4 Chemical seasoning @ 1 o, z, natural spices! 0.2 it 100 20.0 To mix the above raw materials, cut the semi-thawed walleye surimi into approximately 1 cm squares, then cut them into pieces with a food cutter, then transfer them to a sieve machine and add the other raw materials one by one. The mixture was kneaded for 20 minutes.
(2)エクストルージ五ン拳クツキングの条件使用した
エクストルーダー:
二軸型同方向回転方式、
内径46ffJ+1スクリュー長さ690IIIISL
力=15ノズル:
開口部厚み0.8朋、×巾50順
開口部深さ101顛
エクストルーダーの操作条件:
原料供給量1000 El / winスクリュースピ
ード100 r*pJ
シリンダー内温度内温力条件:
原料投入口付近の温度 20”C原料が
200 jlJl程度搬送された付近の温度80’C原
料が430鴎程度搬送された付近の温度110℃原料が
600B程度搬送された付近の温度130°Cスクリュ
ーの末端付近の温度 150°Cスクリューの
末端付近の圧力 15 K9/d製品のカットサ
イズ 1001111(3)製品の品質と
出来高
製品の巾52j111.厚み1.2m、乳黄色、不透明
でスライスチーズ様の柔軟性あるシート状食品素材で、
水分含量39.0%、水分活性(Ay)値は0.886
で、出来高は19.8に9であった。(2) Extrusion conditions
Force = 15 Nozzle: Opening thickness 0.8 mm, width 50 mm, opening depth 101 mm Extruder operating conditions: Raw material supply amount 1000 El/win Screw speed 100 r*pJ Cylinder temperature internal temperature conditions: Temperature near the raw material inlet: 20'C Temperature near where the raw material was conveyed about 200 JlJl 80'C Temperature near where the raw material was conveyed about 430 degrees Celsius Temperature near the raw material was conveyed about 600 B 130°C Temperature near the end of the screw 150°C Pressure near the end of the screw 15 K9/d Product cut size 1001111 (3) Product quality and yield Product width 52J111. Thickness 1.2 m, milky yellow, opaque, sliced cheese-like. A flexible sheet food material,
Moisture content 39.0%, water activity (Ay) value 0.886
So, the trading volume was 19.8 to 9.
(4)本製品の食材としての利用
本製品20枚を取り出し、1枚毎に野菜サラダ209宛
を巻き込んだ食品とした。この食品を10名の社員で試
食した結果、スライスチーズよりも弾力性を有し、充分
にこの食品素材として利用出来るという評価が得られた
。(4) Use of this product as a food ingredient 20 pieces of this product were taken out, and each piece was made into a food by incorporating vegetable salad 209 into it. Ten employees tasted this food and found that it had more elasticity than sliced cheese and could be used as a food ingredient.
実施例 2
(1)原材料の配合割合および混合法は下記のように実
施した。Example 2 (1) The blending ratio of raw materials and the mixing method were as follows.
原 材 @ 8合割合 配合重量むきえびペース
ト 35.0% 7.0Kll薄刃小麦粉
37.5 7・5水飴 IQ、0 2.0
大豆レシチン 5.0 1.0植物性マーガ
リン 2.0 0.4食塩 2.0 0.4
化学調味料 2.0 0.4天然香辛料
!・OO・2
天然岩色色素 Q、5 0.1プルラン
5.0 1.0″ij 1
00.0 20・0原材料の混合は、冷凍むきえび
をフードカッターで細切し、これをらいかい機に啓して
混練りしてペースト化し、順次他の原材料を加えて20
分間混練りした。Raw materials @8 ratio Mixed weight Peeled shrimp paste 35.0% 7.0Kll thin blade flour
37.5 7.5 Starch syrup IQ, 0 2.0 Soy lecithin 5.0 1.0 Vegetable margarine 2.0 0.4 Salt 2.0 0.4 Chemical seasonings 2.0 0.4 Natural spices
!・OO・2 Natural rock color pigment Q, 5 0.1 Pullulan
5.0 1.0″ij 1
00.0 20.0 To mix the raw materials, cut the frozen peeled shrimp into small pieces using a food cutter, put this into a peeler, knead it to make a paste, and then add other raw materials one by one.
Kneaded for a minute.
(2)エクストルーダーン・クツキングの条件使用した
エクストルーダー:
二軸型同方向回転方式
内径46u1スクリュー長さ690mm、い=15ノズ
ル:
開口部厚み1・0II11×巾70目
開口部深さ101 am
エクストルーダーの操作条件:
原材料供給量12001 / win
スクリュースピード110 r、p、+。(2) Conditions for extruder and shoeking Extruder used: Two-shaft co-rotating system Internal diameter 46u1 Screw length 690mm, Nozzle: Opening thickness 1.0 II 11 x width 70 opening depth 101 am Extruder operating conditions: Raw material feed rate 12001/win Screw speed 110 r, p, +.
シリンダー内温度、圧力条件:
原料投入口付近の温度 20’(:原料
が200朋程度搬送された付近の温度80’C原料が4
30顛程度搬送された付近の温度120’(:原料が6
oom糧度搬送された付近の温度140°Cスクリュー
の末端付近の温度 150°Cスクリューの末
端付近の圧力 t7Kg/c++!製品のカットサ
イズ 100B(3ン製品の品質と出来高
製品の巾75朋、厚み1.6朋、淡肛色、不透明でスラ
イスハム様の柔軟性あるシート状食品素材で、水分含量
37.6%、水分活性(Av)値Q、 90で、出来高
19.5に9であった。Temperature and pressure conditions inside the cylinder: Temperature near the raw material inlet: 20'C
The temperature near the area where about 30 pieces were transported was 120' (: the raw material was 6
oom Temperature near the conveyed temperature 140°C Temperature near the end of the screw 150°C Pressure near the end of the screw t7Kg/c++! Product cut size: 100B (3mm) Product quality and yield Product width: 75mm, thickness: 1.6mm, light color, opaque, flexible sheet-like food material similar to sliced ham, moisture content: 37.6% The water activity (Av) value Q was 90, and the yield was 19.5 to 9.
(4)本製品の食材としての利用
本製品を20枚取り出し、巾75間、長さ105鴎、厚
さ10朋にカットしたスライスパン40枚を用意し、ス
ライスパン2枚の間に本製品1枚づつを挟み、この食品
を社員10名で試食した結果、スライスハムに等しい弾
力性を有し、えび特有の風味があり、充分この食品素材
として利用出来るという評価が得られた。(4) Use of this product as a food ingredient Take 20 slices of this product and prepare 40 slices of bread cut into 75 mm wide, 105 mm long, and 10 mm thick, and place this product between 2 slices of bread. As a result of tasting the food with 10 employees, one by one, they found that it had the same elasticity as sliced ham and the unique flavor of shrimp, making it suitable for use as a food ingredient.
実施例 3
(1)原材料の配合割合および混合法は下記のように実
施した。Example 3 (1) The blending ratio of raw materials and the mixing method were as follows.
原 材 料 配合割合 配合重量豚ひき
聞 20% 4・OK9強力小
麦粉 37 7.4小麦澱粉
10 2.0大豆蛋白
81.6大豆レシチン
51.0グリセリン 10 2.
0食塩 20.4
化学調味料 10.2天然香辛料
1 0.2ビーフエキス
20・4ソルビタン脂肪酸エステル 1
0+2天然色素 10.2血液
プラズマ蛋白 20.4Wt100
2Q、0
原材料の混合は、豚ひき肉に大豆レシチン、グリセリン
、ビーフェキスを加えてらいかい機で10分間混練りし
、次いでその他の原材料を順次添加して、20分間混練
りした。Ingredients Mixing ratio Mixing weight Pork mince 20% 4.OK9 strong wheat flour 37 7.4 Wheat starch
10 2.0 soy protein
81.6 Soy lecithin
51.0 Glycerin 10 2.
0 Salt 20.4 Chemical seasonings 10.2 Natural spices
1 0.2 beef extract
20.4 sorbitan fatty acid ester 1
0+2 Natural pigment 10.2 Blood plasma protein 20.4Wt100
2Q, 0 The raw materials were mixed by adding soybean lecithin, glycerin, and Beefex to minced pork and kneading them for 10 minutes using a rice cake machine, and then sequentially adding the other raw materials and kneading them for 20 minutes.
(2)エクストルージョン・クツキングの条件使用した
エクストルーダー:
二軸型同方向回転方式
内径46朋、スクリュー長さ690順、い=15ノズル
:
開口部厚み1.2fl×巾50朋
開口部深さ10!龍
エクストルーダーの操作条件:
原材料供給f11980 g/ +minスクリュース
ピード80 r、pallシリンダー内温度内温力条件
:
原ト投入a付近の温度 20’C原料が
200順程度搬送された付近の温度 80℃原料が43
0龍程度搬送された付近の温度110℃原料が600j
Im程度搬送された付近の温度150℃スクリューの末
端付近の温度 160’Cスクリユーの末端付
近の圧力 14 K9/ crlt製品のカットサ
イズ 120sn(3)製品の品質と出来
高
製品の巾55朋、厚み1・6m、獣肉の加熱した色調を
呈し、不透明でやや硬いシート状食品素材で、水分含量
30・o96、水分活性(Ay)値は0.85で、出来
高19.7に9であった。(2) Extrusion and shoeking conditions Extruder used: Two-shaft co-rotating system Inner diameter 46 mm, screw length 690 mm, I = 15 Nozzle: Opening thickness 1.2 fl x width 50 mm Opening depth 10! Operating conditions of the Dragon extruder: Raw material supply f11980 g/+min Screw speed 80 r, Pall temperature inside the cylinder Temperature conditions: Temperature near raw material input a: 20'C Temperature near where raw material is conveyed for about 200 rounds: 80°C 43 raw materials
The raw material at a temperature of 110℃ near where it was transported was 600J
Temperature near the end of the screw 160'C Pressure near the end of the screw 14 K9/crlt Product cut size 120sn (3) Product quality and output Product width 55 mm, thickness 1・6m, an opaque and slightly hard sheet-like food material with the color tone of cooked meat, moisture content 30.o96, water activity (Ay) value 0.85, yield 19.7.9.
(4)本製品の食材としての利用
本製品20枚を取り出し、P!B騰水中水中分間浸漬し
た後取り出し、食用油をひいたフライパンを160℃に
加熱し、その上で本製品を上下2分間ずつ焙焼した。こ
の焙焼品を10名の社員で試食した結果、ハンバーグを
簿切りして焙焼したような香味と旨味を有し、充分に副
食として利用出来るという評価を得た。(4) Use of this product as food Take out 20 pieces of this product and P! After being immersed in B-soaked water for a minute, the product was taken out, and a frying pan coated with edible oil was heated to 160°C, and the product was roasted on top and bottom for 2 minutes each. As a result of tasting this roasted product with 10 employees, it was evaluated that it had a flavor and flavor similar to that of a roasted hamburger steak, and that it could be used as a side dish.
Claims (8)
油脂類、可塑剤、調味料、香辛料、着色料、着香料を副
原料として、エクストルージョン・クッキング工程を経
て製造されるシート状食品素材。(1) Sheet-shaped food produced through an extrusion cooking process using animal and vegetable protein and starch as the main ingredients, and animal and vegetable oils and fats, plasticizers, seasonings, spices, colorants, and flavorings as secondary ingredients. material.
、魚肉落し身、血液プラズマ蛋白質等で構成される特許
請求の範囲第1項に記載のシート状食品素材。(2) The sheet-shaped food material according to claim 1, wherein the animal and vegetable protein used as the main raw material is composed of ground fish, ground fish, blood plasma protein, etc.
類細断物で構成される特許請求の範囲第1項に記載のシ
ート状食品素材。(3) The sheet-like food material according to claim 1, wherein the main raw material animal and vegetable protein is seafood paste or shredded seafood.
肉ひき肉で構成される特許請求の範囲第1項に記載のシ
ート状食品素材。(4) The sheet-like food material according to claim 1, wherein the animal and vegetable proteins as the main raw materials are animal and poultry paste and animal and poultry minced meat.
〜第4項に記載するもののうち、一種または二種以上混
合されたもので構成される特許請求の範囲第1項に記載
のシート状食品素材。(5) The animal and vegetable protein as set forth in claim 1, which is a main raw material, is composed of one or a mixture of two or more of the proteins listed in claims 2 to 4. Sheet food material.
のうち、一種または二種以上混合されたもので構成され
る特許請求の範囲第1項に記載のシート状食品素材。(6) The sheet-like food material according to claim 1, wherein the main starch material is one or a mixture of two or more of grain starch, root mass starch, and milled grain flour.
ルラン、脂肪酸エステル類のうち、一種または二種以上
混合されたもので構成される特許請求の範囲第1項に記
載のシート状食品素材。(7) The sheet-like food material according to claim 1, wherein the plasticizer as an auxiliary raw material is composed of one or a mixture of two or more of glycerin, sorbitol, pullulan, and fatty acid esters.
燐脂質のうち、一種または二種以上混合されたもので構
成される特許請求の範囲第1項に記載のシート状食品素
材。(8) The sheet-like food material according to claim 1, wherein the fats and oils as auxiliary raw materials are composed of one or a mixture of two or more of animal and vegetable oils and fats and animal and vegetable phospholipids.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60133098A JPS61293376A (en) | 1985-06-20 | 1985-06-20 | Sheetlike food material produced through extrusion cooking process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60133098A JPS61293376A (en) | 1985-06-20 | 1985-06-20 | Sheetlike food material produced through extrusion cooking process |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61293376A true JPS61293376A (en) | 1986-12-24 |
JPH0139745B2 JPH0139745B2 (en) | 1989-08-23 |
Family
ID=15096779
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60133098A Granted JPS61293376A (en) | 1985-06-20 | 1985-06-20 | Sheetlike food material produced through extrusion cooking process |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61293376A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2678640A1 (en) * | 1991-07-03 | 1993-01-08 | Bourgogne Biodyne | PROCESS FOR THE CONTINUOUS PRODUCTION OF PARTIALLY HYDROLYSIS STARCH PRODUCED BY THIS METHOD AND ITS APPLICATIONS |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61216663A (en) * | 1985-02-20 | 1986-09-26 | Shokuhin Sangyo Ekusutoruujohn Kutsukingu Gijutsu Kenkyu Kumiai | Method of forming fish and shellfish into tissue |
-
1985
- 1985-06-20 JP JP60133098A patent/JPS61293376A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61216663A (en) * | 1985-02-20 | 1986-09-26 | Shokuhin Sangyo Ekusutoruujohn Kutsukingu Gijutsu Kenkyu Kumiai | Method of forming fish and shellfish into tissue |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2678640A1 (en) * | 1991-07-03 | 1993-01-08 | Bourgogne Biodyne | PROCESS FOR THE CONTINUOUS PRODUCTION OF PARTIALLY HYDROLYSIS STARCH PRODUCED BY THIS METHOD AND ITS APPLICATIONS |
WO1993001216A1 (en) * | 1991-07-03 | 1993-01-21 | Biodyne Bourgogne | Method for continuously producing partially hydrolyzed starch, product thereby obtained and uses thereof |
Also Published As
Publication number | Publication date |
---|---|
JPH0139745B2 (en) | 1989-08-23 |
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